EP1218587A1 - Regulation system for the short circulation and headbox of a paper machine or equivalent - Google Patents
Regulation system for the short circulation and headbox of a paper machine or equivalentInfo
- Publication number
- EP1218587A1 EP1218587A1 EP00960725A EP00960725A EP1218587A1 EP 1218587 A1 EP1218587 A1 EP 1218587A1 EP 00960725 A EP00960725 A EP 00960725A EP 00960725 A EP00960725 A EP 00960725A EP 1218587 A1 EP1218587 A1 EP 1218587A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- headbox
- sensors
- fibre
- flow state
- short circulation
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
- D21F1/00—Wet end of machines for making continuous webs of paper
- D21F1/02—Head boxes of Fourdrinier machines
- D21F1/026—Details of the turbulence section
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
- D21F1/00—Wet end of machines for making continuous webs of paper
- D21F1/02—Head boxes of Fourdrinier machines
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
- D21F1/00—Wet end of machines for making continuous webs of paper
- D21F1/66—Pulp catching, de-watering, or recovering; Re-use of pulp-water
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S162/00—Paper making and fiber liberation
- Y10S162/09—Uses for paper making sludge
- Y10S162/10—Computer control of paper making variables
- Y10S162/11—Wet end paper making variables
Definitions
- the present invention relates to a method in the measurement and control of the short circulation and the headbox of a paper machine or equivalent.
- the present invention relates also to a headbox and the short circulation.
- the invention relates to the arrangement of the short circulation and the headbox of a paper machine or equivalent.
- the paper machine or equivalent refers in the present context to a machine with which paper-like product such as paper, board or tissue paper is produced.
- the stock feeding of the paper machine is in general as follows.
- the stock components are stored in the paper mill in separate storage tanks, wherefrom they are fed into proportioning tanks and therefrom further into a common mixing tank, in which the stock components are intermixed.
- the mixing tank the stock is fed into a machine tank, wherefrom the stock, being in general in about 3% consis- tency, is fed into a short-circulation wire pit.
- the thick stock is diluted into a headbox consistency, which is in general about 1%.
- the fibres and fillers to be used as raw material are taken to the wire through a headbox and conveyed by water.
- the filtrate having passed through the wire, containing fibrous agents and fillers in great quantities, is returned as a filtrate of the thick stock from the machine tank back to the wire through the headbox.
- a flow link thus formed is called a short circulation.
- Impurities may enter in the short circulation together with the thick stock or through other ways which have to be removed before the headbox. This is carried out with short-circulation cleaning apparatus, such as hydrocyclones, screens, machine screens and deaeration tanks.
- the short circulation together with the headbox in connection therewith is in general considered as the most sensitive part of the papermaking process. Any small changes in the consistency, flow or other parameters immediately affect the quality of the paper being manufactured or cause web breaks on the paper machine.
- the function of the short circulation in the papermaking is, among other things, to produce a fibre suspension of uniform quality, in which the various components (fibre fractions, chemicals and fillers) are intermixed into a homogeneous fluid. The good homogeneity of the stock thus produced will guarantee a uniform quality in the paper and an undisturbed production process in subsequent phases.
- one of the important functions of the headbox is formation of slice jet to be optimal in its flow state.
- slice jet the solid matter is distributed homogeneously, the floe size is optimal, the disturbances are minimal, and the turbulence level is under control.
- the essential measurable and controlla- ble quantity is the degree of suspension fluidization, illustrating the intermobility of fibres.
- various geometrical designs are used for fluidizing the suspension, such as step changes of flow channels, adjustments of trailing elements and various surface phenomena, such as boundary layer turbulence, wherewith turbulence is generated in the flow of the suspension.
- the stock entering the paper machine is built from a number of separate (2-4) stock components, the fibrous properties of which deviate from each other and vary along with changes of the paper grade to be manufactured.
- the stock components are mixed into homogeneous fluid in so-called mixing reactors located in the parts of the short circulation to which several stock components are brought simultaneously.
- the operation of the OptiFeed process is dependent on the goodness of the opera- tion of the mixing reactor.
- the mixing should be as perfect as possible and in addition, to work for all paper grades being manufactured, even though the flow quantities of different components, depending on the quality, may vary to a great extent.
- the goodness of the mixing of different components being mixed as known in the art can be measured and controlled when an optimal operation is to be secured.
- the mixability of suspensions containing fibrous matter is dependent on the mobility of solid matter and the turbulence generated there- through. Optimizing the generation of turbulence is implementable e.g. by means of various adjustable throttling elements, disclosed e.g. in the patent application of the applicant No. FI-992015.
- the fibres tend to form accumulations called floes. If the consistency of the flow exceeds the sedimentation consistency, the floes are built into a net-like united phase, which in the papermaking is an undesired state.
- the state in which the structure is completely decomposed is called fluidized.
- momentary fluidization of components to be mixed is expected. The mixing is in general carried out by conducting flows of different components into one at different speeds. If the state of fluidization can be monitored, the differential speed required (shearing stress between the flows being mixed) can be set optimal.
- the structure of a fibre net or floes is decomposed.
- the state of fluidization can be estimated with the aid of floe size and its completeness with the aid of the minimum size achieved.
- the floe size measuring in the process circumstances is very difficult in practice.
- Generating turbulence in the fibre suspension causes breaking up of fibre floes and increased intermobility of individual fibres.
- Providing fluidization by in- creasing the turbulence requires geometric changes to add shearing stresses or a surface of a flow channel or a trailing element to produce sufficient boundary- layer turbulence. Increased fluidization as such will not cause reduction of turbulence.
- the fibre suspension usually tends to become re-flocculated so to speak, which can be observed as reduced fibre mobility (degree of fluidization).
- the properties of turbulence include so-called dissipation, which means changing of the kinetic energy of the turbulence into internal energy (heat) of the fluid.
- the degree of fluidization of the suspension will be de- creased owing to the dissipation of turbulence.
- the fluidization of the suspension is a transient state, the follow-up of which is essential for the success of the papermaking process.
- the objective of the present invention is to develop a method and an apparatus for real-time measuring of the short circulation of a paper machine or equivalent and of the fibre mobility of the suspension of the headbox and for controlling the flow state.
- the objective of the present invention is also to provide a method and an apparatus, wherewith as optimal mixability of the fibre suspension as possible is guaranteed in different parts of the short circulation and the headbox so that the fibre suspension is in an optimal state for the subsequent phase of the process.
- the method according to the invention is mainly characterized in that in the method, the selected measurement targets are provided with means for measuring the fibre mobility of the fibre suspension, and on the basis of the fibre mobility measured from the fibre suspension, the flow state of the fibre suspension is controlled..
- the headbox of the invention is in turn characterized in that the headbox comprises sensors on the width of the headbox or a traversing sensor/sensors, being fitted in different width points of the headbox, and that a sensor/sensors is/are arranged to measure the fibre mobility profile of the headbox on the width of the entire headbox and that the headbox comprises means for changing the flow state on the basis of the measurement data obtained from the sensors.
- the short circulation of the invention is characterized in that the short circulation comprises a sensor/sensors, disposed in the pipes of the short circulation and/or in the cleaning apparatus, and that a sensor/sensors are arranged to measure the fibre mobility of the fibre suspension in the short circulation and that the short circula- tion comprises means for changing the flow state on the basis of the measurement data rendered by the sensors.
- the apparatus components used for controlling the mixture in the short circulation of a paper machine or equivalent are provided with sensors measuring the flow state, on the basis of the data obtained wherefrom the flow state is controlled by means of control devices.
- the furnish of the fibre suspension is controlled to be such that it is optimal for the next process phase.
- the solution according to the invention can be used also in cardboard and tissue machines.
- the fibre mobility of the suspension of the headbox can be measured most precisely on the entire width of the slice channel.
- the slice channel is provided with a row of sensors, a sensor matrix or a traversing sensor, in which the degree of fluidization of the suspension is measured in real time.
- a row of sensors or a sensor matrix is positioned on each layer.
- the flow state of the suspension of the headbox is controlled, in order to make the fibre mobility, that is, the degree of fluidization, optimal.
- the optimal range of variation of the fibre mobility is known for different paper grades, the quality of the paper produced can be controlled in changing running circumstances.
- the optimal range of variation of the fibre mobility can be determined experimentally.
- Figure 1 is a principle block diagram representation about measurement and control of solid matter mobility in the short circulation.
- Figure 2 presents development of fibre mobility as a function of residence time t.
- Figure 3 presents a short circulation process arrangement.
- Figure 4A presents an example of the structure of a short circulation mixing reactor.
- Figure 4B presents an actuator for controlling the mixing in a short circulation mixing reactor with the actuator in open position.
- Figure 4C presents the actuator of Fig. 3B in partly closed position.
- Figure 5 presents an example of positioning a sensor matrix of the invention in the slice area of the headbox and the control system of the invention.
- Figures 6A, 6B and 6C present one embodiment of a turbulence adjuster sleeve to be disposed in a flow channel.
- Figures 7A and 7B present a second embodiment of a turbulence adjuster sleeve to be disposed in a flow channel.
- Figure 1 presents a model for optimizing the mixing of fibre suspension.
- Fig. 1 presents a mixing reactor MR equivalent to the part of the short circulation to which one or more components d, C 2 , C 3 , C 4 are supplied to be mixed in the mixing reactor MR into as uniform mixture as possible.
- the fibre properties of the components Ci, C 2 , C 3 , C to be mixed deviate in general from each other and their mutual ratio varies according to the paper grade to be produced.
- the components Ci, C 2 , C 3 , C 4 to be mixed are mixed in a controllable mixing element ME.
- a mixing sensor MS is positioned to measure the homogeneity of the mixture.
- a stock flow mix is obtained, which is controlled so that its furnish is optimal as possible for the subsequent phase of the process.
- a measuring signal Si is obtained which is taken to the mixing control unit MC to send a control signal S to a mix- ing element MR] . In this manner a feedbeck is formed with which the control of the furnish of the invention can be carried out.
- the sensors to be used for measuring a flow state are e.g. rapid pressure sensors measuring pressure variations or surface friction sensors measuring acceleration.
- fibre mobility can be measured, as well as with sensors based on radioactive radiation, microwave measurement or ultrasonic sensors.
- turbulence is brought into a flow state, wherewith the mobility of the fibre suspension is controlled to be optimal.
- the volume being measured from the fibre suspension in a target being measured is tried to be selected so that it is the smallest element in which the fibres and other ingredients are mixed uniformly.
- the size of such volumetric element is dependent, for instance, on the medium length of fibres and its ideal size varies in different parts of the process and is dependent the product being produced.
- Fig. 2 describes the intensity I of the movement of fibres of the fibre suspension, that is, development of the fibre mobility as a function of the residence time t.
- the intensity I of the fibre movement is inversely proportional to the floe volume.
- the graph is divided into four parts, in part 1 of which the fibre mobility of the fibre suspension is presented before fluidization, whereby the floe size is great and the mobility of fibres small.
- the fibre suspension is fluidized, whereby the fibre mobility increases and the floe size reduces. Thereafter, re-flocculation follows in part 3, whereby the fibre mobility reduces as a function of time, until the flow state ends into a saturation state in part 4, in which the fibre mobility no longer significantly diminishes.
- Figure 3 presents a short-circulation process arrangement, in which such process targets are presented in which the measurement and control arrangement of the mixing presented in Fig. 1 can be applied.
- the headbox 10 in short circulation feeds through its slice opening a stock suspension jet into the wire section 100.
- the water collecting apparatus conduct the water discharged through the wire as a flow F 50 into the wire pit 50.
- a fresh stock flow M T is fed, the consistency whereof being in general of the order 3%.
- the fresh stock is diluted into headbox consistency of the order 1%.
- the suction side of a pump 51 is connected to the mixing area 50a of the wire pit 50. From the pressure side of the pump 51 , a stock flow F 60 diluted into the headbox consistency is directed through the hydrocyclones 60 to a deaeration tank 70.
- the air volume prevailing in underpressure is located above the free surface of the stock.
- the height of the stock surface is determined by the overflow 70a of the deaeration tank 70, across which a stock flow F 70 is flowing, from which the air is removed.
- Said stock flow F 0 is conducted to the mixing area 50a of the wire pit 50.
- a return flow F 61 is brought into said mixing area 50a from the accept of the second phase hydrocyclones, and a fresh stock flow M ⁇ .
- a stock flow F 7 ⁇ is conducted to the suction side of the pump 71.
- the pump 71 feeds the inlet stock flow F ⁇ n through the machine screen 80 to the stock inlet header of the head- box 10.
- the bypass F out of the stock inlet header of the headbox 10 is returned to the deaeration tank 70.
- Reject F 8 ⁇ of the machine screen 80 is conducted to treatment of rejects.
- targets appropriate for measuring and controlling the flow state in short circulation are the positions marked in the figure; in position P A in connection with the mixing area 50a of thick stock and wire water, in position P B in connection with the hydrocyclone unit 60, in position P A in connection with the deaeration unit 70, in position P D in connection with the machine screen 80.
- Figure 4A presents a mixing reactor MR, in which the control of the flow state according to the invention is implemented in the short circulation.
- the mixing reactor MR two or more components C ⁇ , C 2 , ..., are brought to be mixed, which are tried to get mixed into as homogeneous stock mix F m ⁇ x as possible.
- Said mix- able components are for instance, thick stock and wire water.
- Figure 4B presents an actuator with which the control of the flow state of the invention can be implemented in mixing reactors MR located in different process phases of the short circulation, in which the components Ci are mixed in the outer pipe ti and the C 2 in the inner pipe t 2 .
- Component Ci is e.g. thick stock and com- ponent C , wire water.
- delta wings d are installed in the outlet end of the inner pipe t] of the mixing reactor, so-called delta wings d, the angle whereof being controllable with an exterior control.
- the outlet end of pipe ti comprises six delta wings d, in the present example, the angle of which is controlled by means of control actuators do There may be also some other number of delta wings d, available. By opening the delta wings d combat the outer flows can be restricted.
- FIG. 4C presents a delta wing structure of the invention, in which the delta wings d, limit more the flow of the inner pipe ti .
- control means can be used for controlling the flow state in the short circulation.
- Such means are for instance controllable pipe expansions positioned before the cleaning units (hydrocyclones, deaeration tanks), in which the diameter of the pipes and or the location of a pipe expansion can be adjusted, and controls to be implemented in the machine screen, in which the wing angle, distance of the wing, pressure and/or speed of rotation can be controlled.
- controllable throttles can be positioned before the cleaning units.
- Figure 5 presents the headbox 10 of a paper or board machine, comprising a stock inlet header J, tube bank 11, an intermediate chamber 12, a turbulence generator 13 and a slice channel 14.
- the headbox 10 is provided with a row of sensors or sensor matrix S ⁇ ,...,S nm , in which the overall number of sensors is n x m.
- the sensors S ⁇ ,...,S nm are attached to the slice channel 14 so that the sensors S extend on the width and length of the slice channel 14.
- the sensors S With the sensors S, the mobility of suspension fibres are measured and the sensors S are positioned preferably at equal distances e.g. 60 mm from each other.
- the sensors S can be positioned on the upper and lower surface of the slice channel in one- layer headboxes. In multi-layer headboxes the sensors S can be positioned on each layer. With one row of sensors, a momentary transverse profile illustrating the mobility of fibres can be measured. Using a sensor matrix, information can be moreover received about the fibre mobility in machine direction.
- the sensors S ⁇ ,...,Snm are attached to e.g. a slice cone, on the surfaces of the trailing elements or the tube bank and measuring signal leads are drawn therefrom to the receiving unit 20 processing the measurement data and transmitting it to the control unit 30 of the headbox. It is also possible to use a traversing sensor which keeps moving in cross-machine direction.
- the mode of operation of the fibre mobility sensors can be based on a number of different quantities.
- the measurement can be performed e.g. on the basis of rapid pressure variations, whereby pressure sensors are used, or one the basis of acceleration, whereby surface friction sensors are used.
- various optical methods e.g. laser Doppler anemometer
- fibre mobility can be measured like with sensors based on radioactive radiation, microwave measurement or ultrasonic measurement.
- turbulence is gener- ated in the flow state, with which the mobility of the fibre suspension is controlled to be optimal.
- the headbox control unit 30 controls the transverse control of turbulence accord- ing to the invention in the headbox.
- turbulence For controlling the turbulence, a plurality of different methods and apparatus are known in the art. In US. patent specification No. 4,133,713, an arrangement is disclosed in which the turbulence is controlled by changing the length of the trailing element. Turbulence can also be generated by means of various geometric designs, such as step changes of flow channels and by means of flow channel surface structure (e.g. surface roughness, materials).
- Figures 6 and 7 present a turbulence adjuster sleeve T to be disposed in the flow channel, wherewith the turbulence is adjusted with two nested sleeves Ti and T so that the inner sleeve T 2 is moved by rotating and/or pushing it relative to the outer sleeve Ti.
- the inner sleeve T 2 has a geometrical form wherewith an abrupt change is produced in the flow state and thus, turbulence at said point.
- Adjuster sleeves T can be positioned e.g. in the channels 13 al l , 13 a ⁇ ,... of the turbulence generator.
- Figure 6 presents more in detail a first way of adjusting the adjuster sleeve T of the invention, in which the flow state is changed by rotating the inner sleeve T 2 .
- Figures 6B and 6C present section C-C of Fig. 6 A, in which the inner sleeve T 2 is adjusted into two different positions for controlling the degree of turbulence.
- Figure 7 presents a second adjustment form of the adjuster sleeve T.
- the sleeve disposed within the flow pipe is moved in machine direction, so that the adjustment is produced in the generation of the turbulence caused by the sleeve.
- Figs. 7A and 7B by pushing the adjuster sleeve T disposed within the flow pipe V into different directions, a change can be produced in the flow state.
- the rotation of the sleeve relative to its axis and/or moving it in machine direction generates controlled changes in the strength and orientation of turbulence.
- control of turbulence intensity is obtained after the turbulence generator, that is at the beginning of the slice channel.
Landscapes
- Paper (AREA)
- Steering-Linkage Mechanisms And Four-Wheel Steering (AREA)
- Train Traffic Observation, Control, And Security (AREA)
Abstract
Description
Claims
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FI992016 | 1999-09-21 | ||
FI992016 | 1999-09-21 | ||
PCT/FI2000/000797 WO2001021885A1 (en) | 1999-09-21 | 2000-09-20 | Regulation system for the short circulation and headbox of a paper machine or equivalent |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1218587A1 true EP1218587A1 (en) | 2002-07-03 |
EP1218587B1 EP1218587B1 (en) | 2006-06-21 |
Family
ID=8555324
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP00960725A Expired - Lifetime EP1218587B1 (en) | 1999-09-21 | 2000-09-20 | Regulation system for the short circulation and headbox of a paper machine or equivalent |
Country Status (7)
Country | Link |
---|---|
US (1) | US6551459B1 (en) |
EP (1) | EP1218587B1 (en) |
JP (1) | JP2003510472A (en) |
AT (1) | ATE331070T1 (en) |
AU (1) | AU7292500A (en) |
DE (1) | DE60028988T2 (en) |
WO (1) | WO2001021885A1 (en) |
Families Citing this family (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ATE331070T1 (en) | 1999-09-21 | 2006-07-15 | Metso Paper Inc | CONTROL SYSTEM FOR SHORT CIRCULATION AND HEADBOX IN A PAPER MACHINE OR THE LIKE |
AU2521001A (en) | 1999-12-30 | 2001-07-16 | Metso Paper Inc. | Method and system for controlling headbox in a paper/board machine |
FI20001405A (en) | 2000-06-13 | 2001-12-14 | Metso Paper Inc | A method for fluidizing fluidized bed flow control apparatus used in a headbox of a papermaking machine or the like and fluidizing fluidization control apparatus |
FI117292B (en) | 2000-06-13 | 2006-08-31 | Metso Paper Inc | Headbox of a paper machine or similar |
FI20002680A0 (en) * | 2000-12-07 | 2000-12-07 | Valmet Corp | A method and apparatus for adjusting the dry matter profile of a web on a wire section of a paper machine / board machine |
EP1342843B1 (en) * | 2002-03-01 | 2007-11-14 | Voith Patent GmbH | Method and system for controlling the web formation |
FI113971B (en) | 2003-02-11 | 2004-07-15 | Metso Paper Inc | Stock treatment apparatus for treatment of stock passed to headbox of paper machine, comprises accept line of hydrocyclone plant and connected with stock line of stock fed from second stock chest |
DE10317720A1 (en) * | 2003-04-17 | 2005-02-17 | Voith Paper Patent Gmbh | headbox |
AT414244B (en) * | 2004-05-13 | 2006-10-15 | Andritz Ag Maschf | METHOD AND DEVICE FOR THE MIXTURE OF SUBSTANCES |
DE102005039304A1 (en) * | 2005-08-19 | 2007-02-22 | Voith Patent Gmbh | Method for controlling at least one property of a fibrous web and associated sheet forming system |
US20090250182A1 (en) * | 2005-10-25 | 2009-10-08 | Sumitomo Seika Chemicals Co., Ltd. | Papermaking Method and Papermaking System |
FI123392B (en) * | 2008-02-22 | 2013-03-28 | Upm Kymmene Oyj | Method for Precipitation of Calcium Carbonate in a Fibrous Web Process and Fiber Machine Machine Approach |
DE102010038694A1 (en) * | 2010-07-30 | 2012-02-02 | Voith Patent Gmbh | constant part |
DE102018120820A1 (en) * | 2018-08-27 | 2020-02-27 | Voith Patent Gmbh | turbulence generator |
Family Cites Families (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3573160A (en) * | 1969-01-29 | 1971-03-30 | Kasimir Lopas | Tapered manifold stock distribution system for a papermaking machine with movable wall therein |
US4133713A (en) | 1977-10-11 | 1979-01-09 | The Procter & Gamble Company | Microturbulence generator for papermachine headbox |
SE421939B (en) * | 1980-06-05 | 1982-02-08 | Karlstad Mekaniska Ab | BACKGROUND MANAGEMENT PROCEDURE |
CH671418A5 (en) | 1987-02-23 | 1989-08-31 | Escher Wyss Gmbh | |
US5812404A (en) * | 1996-04-18 | 1998-09-22 | Valmet Corporation | Method for overall regulation of the headbox of a paper machine or equivalent |
US5944957A (en) * | 1997-03-14 | 1999-08-31 | Valmet Corporation | Regulations system in a paper machine for controlling variation of the basis weight of the paper in the machine direction |
FI974327A (en) * | 1997-11-25 | 1999-05-26 | Valmet Automation Inc | Method and apparatus for adjusting the properties of paper |
FI116075B (en) * | 1998-02-23 | 2005-09-15 | Metso Paper Inc | Paper machine control system |
US6086716A (en) * | 1998-05-11 | 2000-07-11 | Honeywell-Measurex Corporation | Wet end control for papermaking machine |
FI103676B (en) | 1998-06-10 | 1999-08-13 | Metso Paper Inc | Short-circuiting process arrangement for a paper or board machine |
FI982625A (en) * | 1998-12-04 | 2000-06-05 | Valmet Automation Inc | Method and apparatus for adjusting paper properties |
ATE331070T1 (en) | 1999-09-21 | 2006-07-15 | Metso Paper Inc | CONTROL SYSTEM FOR SHORT CIRCULATION AND HEADBOX IN A PAPER MACHINE OR THE LIKE |
-
2000
- 2000-09-20 AT AT00960725T patent/ATE331070T1/en not_active IP Right Cessation
- 2000-09-20 JP JP2001525038A patent/JP2003510472A/en not_active Withdrawn
- 2000-09-20 WO PCT/FI2000/000797 patent/WO2001021885A1/en active IP Right Grant
- 2000-09-20 US US10/088,714 patent/US6551459B1/en not_active Expired - Fee Related
- 2000-09-20 AU AU72925/00A patent/AU7292500A/en not_active Abandoned
- 2000-09-20 EP EP00960725A patent/EP1218587B1/en not_active Expired - Lifetime
- 2000-09-20 DE DE60028988T patent/DE60028988T2/en not_active Expired - Fee Related
Non-Patent Citations (1)
Title |
---|
See references of WO0121885A1 * |
Also Published As
Publication number | Publication date |
---|---|
ATE331070T1 (en) | 2006-07-15 |
JP2003510472A (en) | 2003-03-18 |
DE60028988D1 (en) | 2006-08-03 |
WO2001021885A1 (en) | 2001-03-29 |
US6551459B1 (en) | 2003-04-22 |
EP1218587B1 (en) | 2006-06-21 |
AU7292500A (en) | 2001-04-24 |
DE60028988T2 (en) | 2006-11-09 |
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